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提出了一种新的膜分离过程即非离子W/O型微乳液-中空纤维膜萃取,所用非离子型微乳液体系为(OP-7+OP-4)/苯甲醇/D2EHPA/煤油/盐酸.在不同微乳液流速、料液流速、微乳液内相盐酸浓度、料液浓度、以及不同中空纤维膜数等条件下进行了微乳液-中空纤维膜逆流萃取Nd3+的研究.结果表明,微乳液和料液流速越小,萃取率越高,内相富集倍数越大.微乳液内相盐酸浓度越大,萃取率越高,但富集倍数反而减小.料液初始浓度越小,萃取率和富集倍数越大.当微乳液流速为6 mL/min、料液与微乳液流速比为3∶1、微乳液内相盐酸浓度为4 mol/L、料液浓度为200mg/L时,经过微乳液在三个中空纤维膜萃取器中的串联萃取,Nd3+的萃取率达96.3%,内相Nd3+浓度为4 238 mg/L,是萃余料液浓度的572.7倍,内相富集倍数为21.2.膜萃取过程与膜溶剂萃取相比对Nd3+有更高的萃取效率.

参考文献

[1] Ovejero-Escudero F J;Angelino H;Casamatta G .Microemulsions as adaptive solvents for hydrometallurgical purposes:a preliminary report[J].J Dispersion Sci Technel,1987,8(01):89-108.
[2] Friberg S.Microemulsions[J].J Disp Sci Technol,1985(06):317.
[3] Tondre C;Xenakis A .Use of microemulsions as liquid membranes[J].Faraday Discussions of Chemical Society,1984,77:115-116.
[4] Vijayalakshmi C S;Annapragada A V;Gulari E .Equilibrium extraction and concentration of multivalent metal ion solutions by using Winsor Ⅱ microemulsions[J].Separation Science and Technology,1990,25:717-727.
[5] Wiencek J M;Qutubuddin S .Microemulsion liquid membranes Ⅱ.copper ion removal from buffered and unbuffered aqueous feed[J].Separation Science and Technology,1992,27(11):1408-1422.
[6] Moulik S;Paul B K .Structure,dynamics and transport properties of microemulsions[J].Advances In Colloid and Interface Science,1997,78:171-180.
[7] 徐光宪;袁承业.稀土的溶剂萃取[M].北京:科学出版社,1987:151-172.
[8] 曾平,雷昱,王桂清,余钟芳,李三凤.NH3·H2O皂化P204/煤油体系微乳液(反向胶束)的溶水性能及其对V(Ⅳ)的萃取研究[J].膜科学与技术,1998(05):19-23.
[9] 戴猷元 .膜萃取过程及进展[J].膜科学与技术,1992,12(01):1-7.
[10] 顾忠茂.液膜分离技术进展[J].膜科学与技术,2003(04):214-223,233.
[11] Raghuraman B;Wiencek J .Extraction with emulsion liquid membrane in a hollow-fiber contactor[J].AICHE Journal,1993,39(11):1885-1889.
[12] 龚福忠,李成海,马培华,唐艳霞,刘经伟.微乳液膜法萃取钕[J].化工学报,2003(11):1569-1574.
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